Introduction
[0001] In today's industries the fabrication of complicated geometrical shapes is typically
made with the aid of computer aided design, (CAD). With Solid Freeform Fabrication,
(SFF) also called rapid prototyping, (RP) one can utilize CAD models to create physical
objects through a layer by layer technique, where a highly intricate 3D model becomes
segmented into thin 2D slices and thereby feasible to be constructed with the aid
of 3D printers.
[0002] Manufacturing by 3D printing is one step closer to having finished goods directly
from digital data, eliminating time staking and costly tooling. Since it is an additive
manufacturing process it does not generate waste as is common in subtractive machining.
Various objects can be manufactured from the same stock of powder, little labor and
skills are required for multi-part designs, and full creation by digital information
reduces risk for human error.
[0003] Today, many different manufacturing methods are employed, including Fused Deposition
Modelling (FDM), Direct Ink Writing (DIW), Inkjet 3D Printing, Selective Laser Sintering
(SLS), Electron Beam Melting (EBM), Selective Laser Melting (SLM), Laminated Object
Manufacturing (LOM), Directed Energy Deposition (DED) and Electron Beam Free Form
Fabrication (EBF). Each method has its own advantages and disadvantages, in particular
with regard to the obtained resolution, the materials that can be employed, manufacturing
time, equipment costs, etc.
[0004] 3D printing takes on where other manufacturing processes fail to deliver. As a layer-by-layer
method it is the main technique to successfully produce complex shaped components
from a sinterable material, such as metal powder. A particular type of 3D printing
is a Powder Bed and Inkjet head 3D printing method (Inkjet printing on a powder bed,
hereinafter referred to as 3DP).
[0005] In this method, a powder layer is spread over a build platform. The powder is then
selectively covered by a liquid binder composition (also named "ink"), which is ejected
from an inkjet head and contains a binder component, which is often a polymer. Typically,
heat is applied on the platform in order to evaporate the solvent (typically water
or another low temperature-boiling solvent, such as methanol, ethanol, or acetone)
in the ink, leaving almost only the binder component. A new powder layer is applied,
and the process is repeated. The placement of the binder/ink determines the final
geometrical shape of the component, where additionally shrinkage needs to be considered
when sintering of the component is needed. When the printing step is finished a drying/curing
step is performed in order to evaporate the solvent and let the 3D-printed parts harden
into said shape. This process is illustrated in Figure 1.
[0006] Subsequently, excess particles (not bound by the "ink") are removed, e.g. by blowing
air or careful removal by hand using a soft brush or similar, and the so-called "green
part" is obtained. This green part is then subjected to a step of removing the binder
component (so-called "debinding"), which is typically effected by heat treatment leading
to thermal decomposition or evaporation of the binder component, leaving the so-called
"brown part". Other treatments may also be contemplated, such as catalytic removal
or solvent extraction, but removal by heat treatment is preferred. Generally, this
is followed by a sintering step in order to fuse the particles' boundaries, giving
the final part. This method can be applied to form full-metal parts made from e.g.
stainless steel. This technology is already put to market and used for the manufacture
of consumer goods, e.g. by Digital Metal AB.
[0007] When it comes to printing with the 3DP technique, the stability of the green part
is critical when producing delicate structures. This is due to the fact that for the
debinding treatment, the green part must be removed from the 3D printer unit and must
be put in e.g. an oven in order to effect thermal debinding. Hence, a high Green Strength
(strength of the green part) is required for certain structures.
[0008] To make 3DP a better competitive alternative to for example the SLS technique, the
Green Strength needs to be increased in order to push the dimension limit to even
more delicate structures than what is possible today.
[0009] Further, it is desired than an improvement in Green Strength can be obtained without
requiring changes to the actual manufacturing process, which is well established.
This implies, as one example, that the viscosity of the binder composition/ink can
remain unaltered, as an increase or decrease in viscosity are expected to cause problems
with currently used inkjet heads and may impair product quality.
Problem to be Solved
[0010] It is an object of the present invention to provide means for increasing the Green
Strength of a green part obtained during a 3DP process.
[0011] It is a further object of the present invention to provide particles suitable for
use in a 3DP process that allow increasing the Green Strength beyond the Green Strength
currently obtainable, preferably without requiring further adaptations to the 3DP
process.
[0012] It is a further object of the present invention to provide particles suitable for
use in a 3DP process that allow adjusting the Green Strength of the green part by
increasing the amount of binder composition/ink, thereby increasing the versatility
of the particles.
[0013] It is a further object of the present invention to provide particles suitable for
use in a 3DP method that have protection against outer influences and are less prone
to surface reactions such as oxidation, without the need for deprotection steps prior
to the use of the particles.
[0014] It is a further object of the present invention to provide a 3DP manufacturing process
allowing to obtain a higher Green Strength of the green part while still allowing
to obtain a good quality final product.
[0015] In the art, aspects of the above problems to be solved have been addressed, in particular
in the following documents:
WO 2016/068899 A1, wherein according to the abstract is taught: "A three-dimensional (3D) printing
method, a build material (consisting of an inorganic particle and a polymer attached
thereto) is applied. The polymer is a continuous coating having a thickness from about
3 nm to about 1500 nm, or nano-beads having an average diameter from about 3 nm to
about 1500 nm."
[0016] US 6048954, wherein according to the abstract is taught: "The development of polymer binder
compositions that provide novel binders for high temperature inorganic particulates,
especially metal and ceramic particulates is described. These materials are especially
useful in a laser beam sintering process known as SLSTM that forms accurately shaped
high strength green objects."
[0017] US 5749041, wherein according to the abstract is taught: "A method of fabricating articles,
such as prototype parts and prototype tooling for injection molding. is disclosed.
The method begins with the fabrication of the article in a "green" state by the selective
laser sintering, or another additive thermal process, applied to a composite powder.
Preferably a powder of metal particles coated with a thermoplastic polymer."
[0019] In
WO 2017007011 there is taught in accordance with the abstract: "Provision of a metal fine particle-containing
composition which enables metal parts on electrical components to be joined at a relatively
low temperature, and which achieves a strong joint and leaves little residual organic
matter after joining. The metal fine particle-containing composition contains: metal
fine particles (P1) comprising a metal element (M) having a bulk melting point of
above 420°C, the surface of the particle being at least partially or wholly covered
by a coating substance (C), and the primary particle diameter being 1 to 500nm; a
low melting point metal powder (P2) comprising a metal or an alloy having a bulk melting
point of 420°C or lower; and an activating agent (A) which decomposes and removes
the coating substance (C) from the surface of the metal fine particle (P1)."
Summary of the Disclosure
[0020] The present invention aims at solving some or all of the above objects and provides
particles according to claim 1. Moreover, a use of the particles according to claim
4, a green part according to claim 6 and an additive manufacturing method according
to claim 9 are provided.
[0021] The invention is detailed herein in accordance with the claims as granted.
Brief Description of the Drawings
[0022]
Figure 1 shows a schematic representation of a 3DP method. Herein, an inkjet 1 obtains
the Wetting Ink / Binder composition (solution) from a reservoir and selectively applies
the binder composition / Wetting Ink to a powder bed 2 provided on a build platform
3. Thereby an object / part 4 is formed, wherein the particles of the powder bed are
preliminarily bound together by the Wetting Ink.
Figure 2 shows a schematic representation of the experimental setup for determining
the Green Strength in a 3-point bending test. Herein, h represents the height of the
sample, P represents the force, S represents the distance between the support rollers,
and L denotes the length of the test specimen (corresponding to the width for a square
test specimen).
Definitions
[0023] The following terms will be used in the following detailed description:
The term "polymer" and "polymeric compound" are used synonymously. A polymer or polymeric
compound is generally characterized by comprising 5 or more, typically 10 or more
repeating units derived from the same monomeric compound/monomer. A polymer or polymeric
material generally has a molecular weight of at least 300, typically 1000 or greater.
The polymer may be a homopolymer, a random copolymer, a block copolymer or a mixture
of any of these, unless reference is made to specific forms thereof. The polymer may
be synthesized by any method known in the art, including radical polymerization, cationic
polymerization and anionic polymerization.
[0024] A monomer in the sense of the present invention is typically a molecule of a chemical
species that is capable to react with another molecule of the same chemical species
to form a dimer, which then is able to react with a another molecule of the same chemical
species to form a trimer, etc., to ultimately form a chain wherein 5 or more, preferably
10 or more repeating units derived from the same chemical species are connected to
form a polymer. The group of the monomer molecule capable of reacting with a group
of another monomer molecule to form the polymer chain is not particular limited, and
examples include an ethylenically unsaturated group, an epoxy group, etc. The monomer
may be monofunctional, bifunctional, trifunctional or of higher functionality. Examples
of bifunctional monomers include di(meth)acrylates and compounds possessing both a
carboxylic acid group and an amide group, and examples of trifunctional monomers include
tri(meth)acrylates.
[0025] The term "poly(meth)acrylate" is used to jointly denote polymers derived from methacrylic
acid, acrylic acid and/or their esters, such as methyl methacrylate or butyl acrylate.
The ester residue is preferably a hydrocarbon group having 1 to 20 carbon atoms, more
preferably an alkyl group.
[0026] The term "weight average molecular weight" denotes the weight average molecular weight
determined by a GPC method using polystyrene as standard.
[0027] In the present invention, all physical parameters and properties are measured at
room temperature (20 °C) and at atmospheric pressure (10
5Pa), unless indicated differently. Further, all values given in % generally relate
to % by weight, unless indicated otherwise. Whenever reference is made to a characteristic
or property that needs to be determined by a specific test method, the methods mentioned
in the Examples can be used. This applies in particular to the measurement of the
Green Strength, the amount of polymeric coating, and the particle size.
[0028] The term "sinterable" is used to denote inorganic materials that have a melting point
of 450°C or higher, preferably 500 °C or higher, more preferably 600 °C or higher.
Sinterable materials in this sense include metals, alloys, ceramics, and glasses having
the required melting point. For composites (such as cermet), it would be sufficient
if at least some of the material present on the outside of the particle has a melting
temperature in the above range, so that the particles may bind to each other during
the sintering treatment to form the final sintered body.
[0029] As used herein, the indefinite article "a" indicates one as well as more than one
and does not necessarily limit its reference noun to the singular, unless this is
evident from the context.
[0030] The term and/or means that either all or only one of the elements indicated is present.
For instance, "a and/or b" denotes "only a", or "only b", or "a and b together". In
the case of "only a" the term also covers the possibility that b is absent, i.e. "only
a, but not b".
[0031] The terms "comprising" and "containing" as used herein are intended to be non-exclusive
and open-ended. A composition comprising or containing certain components thus may
comprise other components besides the ones listed. However, the term also includes
the more restrictive meanings "consisting of" and "consisting essentially of". The
term "consisting essentially of" allows for the presence of up to and including 10
weight%, preferably up to and including 5% of materials other than those listed for
the respective composition, which other materials may also be completely absent.
[0032] The term "Green Strength" used in the present invention relates to the Green Strength
of a rectangular test specimen taken from a green part, determined according to the
method specified in the Examples section.
Detailed Description of the Disclosure and the Invention
[0033] The present invention is based on the finding that providing a polymeric coating
on a part or the entirety of the surface of a sinterable core allows increasing the
Green Strength of a green part by increasing the amount of Wetting Ink / liquid binder
composition applied during the manufacturing process of the green part. This allows,
on the one hand, increasing the Green Strength to levels that could not be obtained
with non-coated sinterable particles so far, and, on the other hand, provides particles
with which the Strength of a green body can be adjusted simply by varying the amount
of binder composition / Wetting Ink. As such, the particles of the present invention
are more versatile in this respect as prior art, uncoated particles. Further, the
coating may provide at least partial protection against outer influences and surface
reactions.
[0034] The present invention thus overcomes shortcomings in the prior art, and provides
a new way of improving / modifying the Green Strength of a green part. Without the
need for changing the actual process for producing the green part. This is favorable
from both a technical as well as economic point of view, as existing equipment can
be used without any adjustments. Further, existing processes do not need to be adapted,
provided adaptation was at all technically feasible.
[0035] In this respect, although there have been prior attempts to improve the Green Strength
of a green part, the prior art did not succeed in providing such particles and solving
the problem of providing means for adjusting / increasing the Green Strength of a
green part. Notably, increasing the concentration of polymeric binder in the "ink"
was previously not possible, as this would lead to an increase in the viscosity of
the binder composition / Wetting Ink to be ejected from the print head, which in turn
leads to problems with the inkjet head and impairs the accuracy of the ink deposition,
whereas on the other hand the amount of ink could not simply be increased, as higher
amounts of binder composition / Wetting Ink could not be absorbed by the sinterable
particles.
[0036] Further, as is demonstrated in the Examples and Comparative Examples, simply increasing
the amount of ink for non-coated particles does not at all lead to an increase in
Green Strength, but rather leads to a significant reduction in Green Strength. This
problem is solved by the present invention, wherein the sinterable particles are coated
fully or at least in part by a polymeric coating composition prior to the use in a
3D manufacturing method such as 3DP where additional binder composition/ink is applied
from a print head (see Figure 1).
[0037] The aspects and materials used in the present invention will now be described in
more detail:
Sinterable Core
[0038] The particles of the present disclosure have a sinterable core on which a polymeric
coating is applied on at least a part of surface of the core.
[0039] In accordance with the invention, the sinterable core is a stainless steel core and
the polymeric coating is at least 80% by weight of the polymeric coating of polyvinyl
pyrrolidone.
[0040] Herein, "made of" describes that the particles consist of stainless steel. Unavoidable
impurities may however be present. As such, 95% by weight or more of the core of the
sinterable particles consists of stainless steel, with the remainder being unavoidable
impurities. Preferably, at least 98% by weight or more, and more preferable at least
99% by weight or more of the core of the sinterable particles is formed by the metal,
metal alloy, glass, ceramic material or a mixture thereof.
[0041] The sinterable particles may be of any shape, but spherical particles are preferable.
This is due to the fact that spherical particles have good flow characteristic and
offer high packing density benefiting the strength of the final product.
[0042] The particles of the present disclosure have a polymeric coating on at least a part
of the surface of the sinterable core. The coating contains 80% by weight or more,
more preferably 90% by weight or more, of a polymer, relative to the total weight
of the polymeric coating. In one embodiment, the polymeric coating essentially consists
of or consists of a polymer.
[0043] The polymeric coating is present in an amount of 0.10 to 10.00 % by weight, relative
to the total weight of the particles. If the amount is less than 0.10 %, it has been
found that no significant effect on the capability to modify the Green Strength by
increasing the amount of liquid binder can be obtained. If the amount is higher than
10.00% by weight, the shrinkage during the subsequent sintering tends to become large,
which might impair the product quality in particular with regard to strength and yield
stress. Overall, a high amount of polymeric coating is economically and environmentally
unfavorable.
[0044] The lower amount of the polymeric coating is 0.10% by weight, but more prominent
effects are obtained if the amount is 0.30% by weight or more or 0.50% by weight or
more. Thus, preferably, the lower limit of the amount of a polymeric coating is 0.30%
by weight or more, more preferably 0.50% by weight or more.
[0045] The upper limit of the amount of the polymeric coating is 10.00% by weight, relative
to the total weight of the particles. Yet, in order to reduce the influence on shrinkage,
it is preferable that the amount is 5.00% by weight or less, more preferably 3.00%
by weight or less, further preferably 2.00% by weight or less, still more preferably
1.50% by weight or less.
[0046] The polymer present in the polymeric coating according to the disclosure is polyvinyl
pyrrolidone. It has been found that a relatively low weight average molecular weight
(Mw) is beneficial for obtaining the desired balance of properties, such as good adhesiveness
and good removability by solvent extraction or heat treatment. As such, the weight
average molecular weight of the polymer is between 1,000 and 50,000, with a molecular
weight of 5,000 to 30,000 being preferred. Polyvinyl pyrrolidone (PVP) having a molecular
weight of 1,000 to 50,000, more preferably 2,500 to 40,000, further preferably 5,000
to 30,000, is the polymer for providing the polymeric coating on the surface of the
sinterable stainless steel core of the particles of the present invention.
[0047] The polymeric coating according to the disclosure and the invention may essentially
consist of the polymer, as outlined above. However, it is also possible that additives
are present in the polymeric coating. In particular the presence of a surfactant or
wetting agent can be beneficial, as this is believed to be able to increase the amount
of "ink" that can be absorbed during the production of the green part, which in turn
is believed to increase the Green Strength of the green body. The surfactant can be
any of anionic, cationic and non-ionic, but is preferably non-ionic. The non-ionic
surfactant is preferably a compound or polymer having a (weight average) molecular
weight Mw of 1,000 or less, preferably 500 or less, such as Tego Wet 500 used in the
Examples, as well as alkylene oxide surfactants of the Pluronic
™ series (BASF). The wetting agent is preferably a polyol, such as a sugar alcohol
such as sorbitol, or another polyol such as glycerol, ethylene glycol or propylene
glycol.
[0048] The particle size of the particles of the present invention is not particularly limited,
but needs to be suitable for an additive manufacturing process. As such, the particle
size is preferably such that 95% by weight or more of the particles have a diameter
of 100 µm or less, preferably 72 µm or less, further preferably 50 µm or less, as
determined by a light scattering method described in more detail in the Examples section.
Use of the Particles and Manufacturing Method
[0049] During the use of the particles for forming a green part, a liquid binder composition
("ink") is used to preliminary bind the particles. The liquid binder composition typically
comprises a polymer selected from the same group of polymers as recited above for
the polymer in the polymeric coating of the particles of the present invention. Preferably,
the polymer present in the liquid binder composition ("ink") is of the same type as
the polymer present in the polymeric coating, although this is not a necessity and
the polymers may be of different types. An embodiment in accordance with the invention
wherein the polymers are of the same type would for instance be one wherein both the
polymer in the polymeric coating and the polymer present in the ink are polyvinyl
pyrrolidone, each preferably having a Mw in the range of 1,000 - 50,000, more preferably
5,000 - 30,000. This embodiment can be applied to all kinds of sinterable cores according
to the disclosure, e.g. those made of stainless steel according to the invention.
[0050] Once the green part has been formed by removing excess powder that is not bound by
the ink, it is generally necessary to remove the binder composition together with
the polymeric coating by a so-called "debinding" treatment. This step is as such known
in the art and can be effected by heat treatment, by catalytic decomposition of the
polymer in the polymeric coating and the ink (e.g. by using an acid in case of acid-decomposable
polymers), or by solvent extraction. For this reason, it is generally preferable if
the polymer present in the polymeric coating and/or the ink is water-soluble or soluble
in solvents that are easily removable due to evaporation, such as methanol, ethanol
or acetone. Water-soluble polymers are particularly preferred, also in view of the
manufacturing process, where water-based "inks" and heating are conducted. As such,
preferably one or both of the polymers present in the polymeric coating and/or the
"ink" are water-soluble.
[0051] The debinding can be conducted thermally. Here, the green part is preferably heated
to a temperature in the range of 250 to 500°C. Usually, performing a thermal debinding
treatment for 3 to 10 hours is sufficient for removing the polymer and to form the
brown part. A good debinding can generally be obtained within 6 - 8 hours.
[0052] Subsequent to the formation of the brown part, it is often desired to sinter the
resulting brown part in order to fuse the sinterable particles at their surfaces,
to provide strength and integrity to the resulting product. This is typically conducted
by slowly heating (e.g. at a heating range of 1 to 5°C/minute) the brown part to a
temperature of about 1,000 to 1,500°C for 10 to 20 hours, followed by cooling at moderate
cooling rates (15°C/minute or less).
[0053] The present invention will be demonstrated in more detail by way of the following
Examples. These are however not intended to limit the scope of the present invention
in any way, and the protective scope of the present application is determined solely
by the appended claims.
EXAMPLES
Examples 1 to 9 and Comparative Examples 1 - 3
Preparation of Particles A
[0054] 990 g of gas atomized stainless steel particles 316L (obtainable from Carpenter under
the tradename CarTech
® 316L with the nominal composition, in wt.-%, 0.03 C, 2.00 Mn, 0.045 P, 0.030 S, 1.00
Si, 16.00 - 18.00 Cr, 10.00 - 14.00 Ni, 2.00 - 3.00 Mo, balance Fe) were put in a
mixing chamber and covered with a lid having an opening for the shaft of an overhead
stirrer and an additional opening allowing the addition of liquid.
[0055] Separately, a Coating Solution A was prepared by adding 7.5 g of polyvinyl pyrrolidone
(PVP) having a weight average molecular weight Mw of 25,000 to 50 ml of a solution
of 74.65% water, 12 % triethylene glycol, 5 % 1,2 hexane diol, 3.25 of nonionic surfactant,
5% of PVP with an Mw of 25,000 - 30,000 and 0.1 % of a Cyan dye. The resulting mixture
was stirred to dissolve the PVP in the solution.
[0056] After starting the overhead stirrer, the entire Coating Solution A was slowly added
via the opening in the lid of the mixing chamber. After stirring for about 5 minutes,
the resulting particles to which the Coating Solution A had been added were transferred
to a crucible which was then put into an oven. The particles were dried at 200°C for
3 hours to obtain particles having a sinterable core made of stainless steel which
were covered at least in part by a polymeric coating. The dried particles were then
ground in order to break up any agglomerates that may have formed. Subsequently, the
particles were sieved in order to remove any particles having a size exceeding 71
um.
[0057] Since the Coating Solution A contained 10 g of PVP and the amount of stainless steel
particles was 990 g, the aimed amount of PVP was 1% by weight, relative to the total
of the particles. Due to losses by transfer to the crucible and liquid remaining on
the side walls of the crucible and/or the mixing apparatus, the actual PVP content
was lower and determined to 0.68 wt.-% (see Table 1).
Preparation of Particles A'
[0058] Particles A' were prepared in the same manner as particles A, except for pre-drying
the particles obtained after addition of Coating Solution A for 2 hours at 150°C before
drying at 200°C for 3 hours.
[0059] The resulting particles A' had a lower amount of polymeric coating of 0.51 wt.-%
as compared to Particles A, which can be explained by a higher amount of evaporated
components of the Coating Solution A during the pre-drying as compared to Particles
A.
Preparation of Particles B
[0060] Particles B were produced in the same manner as Particles A, except for using the
Coating Solution B instead of the Coating Solution A. Coating Solution B is a solution
obtained by adding 7.5 g of PVP (Mw=25,000) to 50 ml of a solution of 84.4% water,
10 % ethylene glycol, 5% of PVP with an Mw of 15,000, 0.5 % of Tego Wet
™ 500 (nonionic surfactant, Oxirane 2-methyl-, polymer with oxirane, mono(3,5,5-trimethylhexyl)
ether,
CAS 204336-40-3) and 0.1 % of Acid red dye (
CAS 3734-67-6).
[0061] The amount of polymeric coating was found to be 0.51 wt.-% (see Table 1).
Preparation of Particles B'
[0062] Particles B' were produced in the same manner as Particles A', except for using the
above Coating Solution B instead of the Coating Solution A and performing the pre-drying
at a temperature of 120°C instead of 150°C.
[0063] The amount of polymeric coating was found to be 0.64 wt.-%, indicating that at 120°C
a crosslinking of the components may occur, thereby reducing the amount of evaporated
components during the drying process (see Table 1).
[0064] Incidentally, in the present invention the amount of polymeric coating can be determined
by STA using a STA 449 F3 Jupiter
®, available from Netzsch, following ISO 11357-1:2016 and 11358-1:2014 using an argon
5.0 atmosphere. Particle sizes can be determined by a laser diffraction method using
e.g. a Helos Particle Size Analysis (Sympatec) following SS-ISO 13320-1.
Reference Particles
[0065] As Reference Particles, the gas atomized stainless steel particles 316L (obtainable
from Carpenter under the tradename CarTech
® 316L) were used without any further treatment.
Formation of TRS Bars
[0066] TRS-Bars of 30 mm x 10 mm (length x width) and roughly 6mm high were made in a plastic
mold with the specified dimensions needed for doing three-point bending tests to evaluate
the Green Strength.
[0067] After disposing the particles indicated in Table 1 in bar form, the particles were
preliminary bound together by manually adding a Wetting Ink A or B (binder composition)
as used in a 3DP method, where the binder composition /Wetting Ink is ejected from
a inkjet head on a bed of the particles to form a green part. The addition was effected
with the aid of a variable volume pipette, (Finnpipette F1 Thermo Scientific). The
amount of Wetting Ink for each Example and Comparative Example is indicated in Table
1, as is the composition of the Wetting Inks A and B. These correspond to the solutions
to which PVP was added in the preparation of Coating Solutions A and B.
[0068] After addition of the Wetting Ink, the bars were dried at 200 °C for 3 h in an oven,
and once cooled extracted from the form. Thereafter, Green Strength tests and thermal
analysis (STA) for determining the TRS Bar polymer content.
[0069] STA was performed as outlined above. The Green Strength was evaluated by the following
method:
Determination of Green Strength
[0070] The GS is obtained through a transversal rupture strength (TRS), three-point bend
test, following ISO 3995:1985.
[0071] The specimen (TRS bar) is placed on two supports with a fixed distance, and then
a from above a force is applied on the center of the specimen. The maximum force applied
before sample failure is registered as the Green Strength. As the specimen (TRS bar)
is rectangular, the formula shown below can be used to obtain the maximum Green Srength:

where the expressions have the following meanings (see also Figure 2) :
GS : Green Strength (MPa)
P : Force (N)
S = length between support rollers (in mm)
h : height of specimen (in mm)
b : width of the specimen (in mm) (equivalent to L in Figure 2 for square test specimen).
[0072] In order to determine the Green Strength, the dimensions of the TRS bars were measured.
The TRS Bars were afterwards tested in a three-point bending machine, following ISO
3995:1985. The force signal was received by a Force transducer (TH-UM T-Hydronics
Inc), and registered by a force indicator (Nobel Elektronik BKI-5).
[0073] The materials and results are summarized in the following Table 1:
Table 1
| Example |
Particles |
Coating Solution Type |
Amount of polymeric coating (wt. %) |
Wetting Ink |
Wetting amount (ml) |
TRS Bar polymer content (wt %) |
Green Strength (MPa) |
| Example 1 |
A |
A |
0.68 |
A |
0.63 |
1.03 |
2.1 |
| Example 2 |
A |
A |
0.68 |
A |
1.26 |
1.29 |
3.9 |
| Example 3 |
A |
A |
0.68 |
B |
0.63 |
0.97 |
1.5 |
| Example 4 |
A |
A |
0.68 |
B |
1.26 |
1.17 |
4.4 |
| Example 5 |
B' |
B |
0.64 |
B |
1.26 |
1.27 |
3.3 |
| Example 6 |
A' |
A |
0.51 |
A |
1.26 |
1.17 |
3.3 |
| Example 7 |
A' |
A |
0.51 |
B |
1.26 |
1.06 |
3.2 |
| Example 8 |
B |
B |
0.51 |
A |
1.26 |
1.22 |
4.3 |
| Example 9 |
B |
B |
0.51 |
B |
1.26 |
0.82 |
4.3 |
| Comparative Ex. 1 |
Reference |
n.a. |
0 |
A |
0.63 |
0.19 |
2.7 |
| Comparative Ex. 2 |
Reference |
n.a. |
0 |
A |
1.26 |
0.41 |
0.7 |
| Comparative Ex. 3 |
Reference |
n.a. |
0 |
B |
1.26 |
0.43 |
1.8 |
Coating Solution Type A:
A solution prepared by adding 7.5 g of PVP (Mw=25,000) to 50 ml of a solution of 74.65%
water, 12 % triethylene glycol, 5 % 1,2 hexane diol, 3.25 of nonionic surfactant,
5% of PVP with an Mw of 25,000 - 30,000 and 0.1 % of a Cyan dye
Coating Solution Type B:
A solution prepared by adding 7.5 g of PVP (Mw=25,000) to 50 ml of a solution of 84.4%
water, 10 % ethylene glycol, 5% of PVP with an Mw of 15,000, 0.5 % of Tego Wet™ 500 (nonionic surfactant, Oxirane 2-methyl-, polymer with oxirane, mono(3,5,5-trimethylhexyl)
ether, CAS 204336-40-3) and 0.1 % of Acid red dye (CAS 3734-67-6)
Wetting ink A:
74.65% water, 12 % triethylene glycol, 5 % 1,2 hexane diol, 3.25 of nonionic surfactant,
5% of PVP with an Mw of 25,000 - 30,000 and 0.1 % of a Cyan dye
Wetting ink B:
84.4% water, 10 % ethylene glycol, 5% of PVP with an Mw of 15,000, 0.5 % of Tego Wet™ 500 (nonionic surfactant, Oxirane 2-methyl-, polymer with oxirane, mono(3,5,5-trimethylhexyl)
ether, CAS 204336-40-3) and 0.1 % of Acid red dye (CAS 3734-67-6)
[0074] The following can be derived from the results provided in Table 1:
Comparative Example 1 using the Reference Particles (not surface-coated) leads to
a Green Strength of 2.7 MPa. This is sufficient for many applications, but is insufficient
in case of thin or delicate structures, as here there is an increasing risk of deformation
or breaking of the green part upon removal from the powder bed 3D-printer processing
unit. Further, the particles are not protected on their surface, which may lead to
surface alterations upon storage of the particles between the production and the 3D-manufacturing
process.
[0075] An attempt to increase the Green Strength of the green part by increasing the amount
of Wetting Ink (binder composition for forming the green part) failed. Rather, the
Green Strength was lowered from 2.7 MPa in Comparative Example 1 to 1.7 MPa in Comparative
Example 2. This shows that an increase of the Green Strength cannot be obtained for
non-coated polymer particles by simply increasing the amount of binder/Wetting Ink.
In fact, the Green Strength is significantly lower in Comparative Example 2.
[0076] The same result was also obtained when instead another type of Wetting Ink (Wetting
Ink B) was used. While the Green Strength is higher as compared to Comparative Example
2, still in Comparative Example 3 the Green Strength is below the Green Strength obtained
with a low amount of Wetting Ink (0.63 ml), as obtained in Comparative Example 1.
Comparative Examples 2 and 3 thus show that the Green Strength of a non-coated particle
cannot be increased by increasing the amount of Wetting Ink, but that instead a decrease
of the Green Strength is actually obtained.
[0077] Example 1 was performed in the same manner as Comparative Example 1, except that
the coated particles A were used. The amount of Wetting Ink was however identical.
Example 1 led to a Green Strength of 2.1 MPa, which is sufficient for many applications,
e.g. for the preparation of solid structures requiring no extremely high Green Strength.
[0078] Example 2 corresponds exactly to Example 1, except that the amount of Wetting Ink
was doubled to 1.26 ml. Contrary to the result obtained in Comparative Example 2,
however thereby a significant increase of the Green Strength to 3.9 MPa could be obtained.
This shows that the particles of the invention are more versatile in that they allow
increasing the Green Strength by simply increasing the amount of Wetting Ink, contrary
to the non-coated Reference Particles.
[0079] The same trend was obtained in Example 3. Here, an amount of Wetting Ink of 0.63
ml led to a Green Strength of 1.5 MPa, which is sufficient for solid objects not requiring
a high Green Strength. Again, by increasing the amount of Wetting Ink to 1.26 ml,
the Green Strength could be raised to 4.4 MPa. Examples 3 and 4 thus confirm the results
of Examples 1 and 2, even if the Wetting Ink A is replaced by Wetting Ink B.
[0080] Examples 5 to 9 also confirm the results obtained in Examples 1 to 4 in that an increase
of the amount of Wetting Ink leads to a significant increase in Green Strength to
at least 3 MPa. Although the reason for this is not clear, a comparison of Examples
4 to 9 reveals that the particles A and B generally lead to a higher Green Strength
as compared to the particles A' and B'. The differences between these particles is
only that the drying of the coating solution was done with a preliminary drying step
at 120 or 150°C for 2 hours prior to drying at 200°C for 3 hours. It appears that
a rapid drying treatment, without a preliminary drying, leads to a different surface
structure, possibly due to crosslinking of the polymer in the coating, which subsequently
leads to a higher Green Strength. In this respect, it is noteworthy that the Green
Strength obtained in Examples 2, 4, 8 and 9 was 3.9 MPa or higher, whereas in Examples
5, 6 and 7 (using the particles A' or B') the Green Strength was in the order of 3.2
to 3.3 MPa.
EXAMPLES 10-13
[0081] Polymer Particles C and D were prepared in a similar manner as Polymer Particles
A and B, except that the amount of PVP (Mw of 25,000) added to the coating solutions
A/B was increased to reach a theoretical PVP content of not 1% by weight (as for Particles
A and B), but of 2% by weight. The amount of 316L stainless steel particles was thus
reduced to 980 g.
[0082] Additionally, the mixing process was altered by using a "Cyclomix high shear impact
mixer", (Hosokava Micron B.V.). The mixer has a capacity of around 10 kg, vacuum can
be applied during mixing and heating up to 150 °C of the mixing chamber is possible.
The rotation speed can be varied between 60-1750 rpm.
[0083] For Particles D using coating solution B', not only the amount of PVP was increased
as compared to coating solution B, but also surfactant content was increased to 2,5%
(Tego Wet), and an additional surfactant was added in an amount of 2.5 % (BYK DYNWET
™ 800 N, an alcohol alkoxylate).The exact compositions of the coating solutions A'
and B' are given below Table 2.
[0084] The mixing process began with introducing all of the 316L SS particles into the mixing
chamber. Then, vacuum was applied, mixing started at 160 rpm and heating ramped towards
110 °C. When reaching 110 °C, the mixing and vacuum pump remained active while 20
ml of the premixed coating solution was injected every 5 minutes.
[0085] After having injected all the coating solution, the temperature was increased to
150 °C and kept at this temperature for one hour. Subsequently the vacuum and heating
were discontinued and the coated particles were poured into an iron/steel crucible
that was placed in an oven for drying (3 hours at 200 °C).
[0086] The obtained particles were analyzed with respect to their polymer coating content.
Further, TRS test bars were prepared (green parts) and tested for their Green Strength
and Polymer content, in the same manner as described above for Examples 1 - 9. The
results are summarized in Table 2.
Table 2
| Example |
Particles |
Coating Solution Type |
Amount of polymeric coating (wt. %) |
Wetting Ink |
Wetting amount (ml) |
TRS Bar polymer content (wt %) |
Green Strength (MPa) |
| Example 10 |
C |
A' |
1.24 |
A |
1.26 |
1.90 |
2.7 |
| Example 11 |
C |
A' |
1.24 |
B |
1.26 |
1.78 |
3.5 |
| Example 12 |
D |
B' |
1.01 |
A |
1.26 |
1.52 |
3.0 |
| Example 13 |
D |
B' |
1.01 |
B |
1.26 |
1.39 |
5.0 |
Coating Solution Type A':
A solution prepared by adding 16.25 g of PVP (Mw=25,000) to 50 ml of a solution of
74.65% water, 12 % triethylene glycol, 5 % 1,2 hexane diol, 3.25 of nonionic surfactant,
5% of PVP with an Mw of 25,000 - 30,000 and 0.1 % of a Cyan dye
Coating Solution Type B':
A solution prepared by adding 16.25 g of PVP (Mw=25,000) to 50 ml of a solution of
79.9% water, 10 % ethylene glycol, 5% of PVP with an Mw of 15,000, 2.5 % of Tego Wet™ 500 (nonionic surfactant, Oxirane 2-methyl-, polymer with oxirane, mono(3,5,5-trimethylhexyl)
ether, CAS 204336-40-3), 2.5 % of BYK DYNWET 800 N and 0.1 % of Acid red dye (CAS 3734-67-6)
Wetting ink A:
74.65% water, 12 % triethylene glycol, 5 % 1,2 hexane diol, 3.25 of nonionic surfactant,
5% of PVP with an Mw of 25,000 - 30,000 and 0.1 % of a Cyan dye
Wetting ink B:
84.4% water, 10 % ethylene glycol, 5% of PVP with an Mw of 15,000, 0.5 % of Tego Wet™ 500 (nonionic surfactant, Oxirane 2-methyl-, polymer with oxirane, mono(3,5,5-trimethylhexyl)
ether, CAS 204336-40-3) and 0.1 % of Acid red dye (CAS 3734-67-6)
[0087] Further tests were conducted in order to evaluate whether the increased amount of
polymer in the green parts led to any problems or high porosity in the final object.
For this test, cubes of 11 × 11 × 7 mm were printed using the 3D printer (Digital
Metal P0601) from the Reference Particles using Wetting Ink A indicated in Table 2
(Reference Cube), as well as Particles C using Wetting Ink A (Cube A) and Wetting
Ink B (Cube B). The green parts were thermally debound (350 °C for 180 minutes) and
sintered (Temperature Profile: temperature increase to 1100°C at 3°C/minute, holding
time of 15 minutes, temperature increase at 3°C/minute to 1360°C, holding time of
120 minutes, temperature decrease at 2°C/minute to 1060°C, holding time of 240 minutes,
and temperature decrease at 10°C/minute to room temperature), and the relative density
(as compared to bulk stainless steel) was determined.
[0088] The Reference Particles (non-coated) achieved a relative density of 97.8%. While
the relative density of the test cubes A and B obtained from the particles of the
invention was expectedly somewhat lower in view of the increased volume of polymer
that may not fully be filled by particle core material during debinding and sintering,
nonetheless very good relative densities of 97,3 % (Cube A) and 97.5 % (Cube B) were
obtained.
[0089] Further, the average shrinkage during sintering was determined. For the Reference
Powder, an average shrinkage of 15% was determined, while the particles of the present
invention led to average shrinkages of between 18 % (Cube A) and 24 % (Cube B). This
shows that the increase in Green Strength is accompanied by only small to moderate
increases in the shrinkage and small to moderate reductions in the relative density.